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阐述了化工过程中真空系统的选型设计与计算方法,并对真空泵选型设计提出一些建议。结合工程应用实例,验证了设计计算方法的可行性。 相似文献
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The location of the reaction zone in the catalytic membrane contactor was determined for two-phase reaction system. As a model reaction oxidation of formic acid by Pt catalyst deposited in the ceramic membrane filtration layer was used. It was determined from gas–liquid mass transport experiments that at gas side overpressures from 0.5 to 0.9 bar the liquid was displaced from membrane support layer and that the tortuosity factor of membrane filtration layer is 3.1. It was estimated on the basis of CO2 fluxes that the reaction zone is close to gas–liquid interface and that the locus of the reaction zone matches with O2 penetration depth calculated on the basis of formic acid disappearance rate. It was also shown that partition coefficient of formic acid in the membrane filtration layer is higher than 1, otherwise formic acid could not migrate to the reaction zone. Only a small fraction of the catalyst was involved in the reaction. The apparent activation energy was estimated to be around 44 kJ/mol. 相似文献
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Yanli Liang Zhan Wang Xiao Ye Wenjuan Li Xuejie Xi Liying Yang Xiuyan Wang Jing Zhang Ye Liu Zhiqi Cai 《Desalination》2011,(1):42
In this paper, polyvinylidene fluoride (PVDF)/polymethyl acrilate (PMMA)/cellulose acetate (CA) blend UF membranes were prepared by chemical reaction introduced phase-inversion method. The results of the experiment show that: (1) The membrane pore size distribution is more uniform due to the presence of carbonates or bicarbonates in the coagulation bath; (2) No more than the stoichiometric ratio amount of carbonates or bicarbonates in the coagulation bath can effectively improve the membrane pore size distribution and make the pore size of membrane more uniform; (3) The membrane prepared by carbonates solution as a working solution in coagulation bath possess superior performance than that by bicarbonates. 相似文献